MX155159A - IMPROVEMENTS TO THE PROCESS FOR THE FRACTIONATION OF EXHAUSTED CATALYSTS - Google Patents

IMPROVEMENTS TO THE PROCESS FOR THE FRACTIONATION OF EXHAUSTED CATALYSTS

Info

Publication number
MX155159A
MX155159A MX182350A MX18235080A MX155159A MX 155159 A MX155159 A MX 155159A MX 182350 A MX182350 A MX 182350A MX 18235080 A MX18235080 A MX 18235080A MX 155159 A MX155159 A MX 155159A
Authority
MX
Mexico
Prior art keywords
fractionation
exhausted catalysts
exhausted
catalysts
Prior art date
Application number
MX182350A
Other languages
Spanish (es)
Inventor
Amalesh Kumar Sirkar
Original Assignee
Hydrocarbon Research Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hydrocarbon Research Inc filed Critical Hydrocarbon Research Inc
Publication of MX155159A publication Critical patent/MX155159A/en

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/90—Regeneration or reactivation
    • B01J23/94—Regeneration or reactivation of catalysts comprising metals, oxides or hydroxides of the iron group metals or copper
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28—Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00—Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/62—Washing granular, powdered or lumpy materials; Wet separating by hydraulic classifiers, e.g. of launder, tank, spiral or helical chute concentrator type
    • B03B5/623—Upward current classifiers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
MX182350A 1979-08-21 1980-05-15 IMPROVEMENTS TO THE PROCESS FOR THE FRACTIONATION OF EXHAUSTED CATALYSTS MX155159A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/068,370 US4287088A (en) 1979-08-21 1979-08-21 Multi-stage fluidization and segregation of used catalyst fractions

Publications (1)

Publication Number Publication Date
MX155159A true MX155159A (en) 1988-02-01

Family

ID=22082118

Family Applications (1)

Application Number Title Priority Date Filing Date
MX182350A MX155159A (en) 1979-08-21 1980-05-15 IMPROVEMENTS TO THE PROCESS FOR THE FRACTIONATION OF EXHAUSTED CATALYSTS

Country Status (3)

Country Link
US (1) US4287088A (en)
MX (1) MX155159A (en)
ZA (1) ZA802700B (en)

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU576504B2 (en) * 1983-08-05 1988-09-01 Gnb Batteries Inc. Apparatus and method for separating materials
US4589981A (en) * 1983-12-12 1986-05-20 Joy Manufacturing Company Fluidized bed classifier
US4666588A (en) * 1985-06-19 1987-05-19 Air Products And Chemicals, Inc. Three-phase reactor design and operation
FR2593087B1 (en) * 1986-01-20 1990-09-07 Bp Chimie Sa LIQUID ELUTRIATION OF OLEFIN POLYMERIZATION SOLID CATALYSTS.
US4720473A (en) * 1986-03-10 1988-01-19 Cri International, Inc. Production of improved catalyst-type particles using length and density grading
US5082552A (en) * 1986-03-10 1992-01-21 Cri International, Inc. Hydrotreating with catalyst particles using length and density grading
US4871446A (en) * 1986-09-03 1989-10-03 Mobil Oil Corporation Catalytic cracking process employing mixed catalyst system
US4752375A (en) * 1986-09-03 1988-06-21 Mobil Oil Corporation Single riser fluidized catalytic cracking process utilizing a C3-4 paraffin-rich co-feed and mixed catalyst system
US4861741A (en) * 1986-09-03 1989-08-29 Mobil Oil Corporation Mixed catalyst system and catalytic conversion process employing same
EP0259156A1 (en) * 1986-09-03 1988-03-09 Mobil Oil Corporation Process for fluidized catalytic cracking with reactive fragments
US4802971A (en) * 1986-09-03 1989-02-07 Mobil Oil Corporation Single riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
US4888103A (en) * 1986-09-03 1989-12-19 Herbst Joseph A Process of stripping in a catalytic cracking operation employing a catalyst mixture which includes a shape selective medium pore silicate zeolite component
US4717466A (en) * 1986-09-03 1988-01-05 Mobil Oil Corporation Multiple riser fluidized catalytic cracking process utilizing hydrogen and carbon-hydrogen contributing fragments
US4865718A (en) * 1986-09-03 1989-09-12 Mobil Oil Corporation Maximizing distillate production in a fluid catalytic cracking operation employing a mixed catalyst system
US4830728A (en) * 1986-09-03 1989-05-16 Mobil Oil Corporation Upgrading naphtha in a multiple riser fluid catalytic cracking operation employing a catalyst mixture
US4892643A (en) * 1986-09-03 1990-01-09 Mobil Oil Corporation Upgrading naphtha in a single riser fluidized catalytic cracking operation employing a catalyst mixture
US4874503A (en) * 1988-01-15 1989-10-17 Mobil Oil Corporation Multiple riser fluidized catalytic cracking process employing a mixed catalyst
US5498327A (en) * 1989-07-19 1996-03-12 Stangeland; Bruce E. Catalyst, method and apparatus for an on-stream particle replacement system for countercurrent contact of a gas and liquid feed stream with a packed bed
US5472928A (en) * 1989-07-19 1995-12-05 Scheuerman; Georgieanna L. Catalyst, method and apparatus for an on-stream particle replacement system for countercurrent contact of a gas and liquid feed stream with a packed bed
US5916529A (en) * 1989-07-19 1999-06-29 Chevron U.S.A. Inc Multistage moving-bed hydroprocessing reactor with separate catalyst addition and withdrawal systems for each stage, and method for hydroprocessing a hydrocarbon feed stream
US5492617A (en) * 1989-07-19 1996-02-20 Trimble; Harold J. Apparatus and method for quenching in hydroprocessing of a hydrocarbon feed stream
US5589057A (en) * 1989-07-19 1996-12-31 Chevron U.S.A. Inc. Method for extending the life of hydroprocessing catalyst
US5209840A (en) * 1991-10-02 1993-05-11 Texaco Inc. Separation of active catalyst particles from spent catalyst particles by air elutriation
US5736052A (en) * 1995-11-27 1998-04-07 Framatome Technologies, Inc. Ion exchange resin particle separation system
US5885534A (en) * 1996-03-18 1999-03-23 Chevron U.S.A. Inc. Gas pocket distributor for hydroprocessing a hydrocarbon feed stream
US5879642A (en) * 1996-04-24 1999-03-09 Chevron U.S.A. Inc. Fixed bed reactor assembly having a guard catalyst bed
EP3083084A4 (en) * 2013-12-18 2017-08-16 United Technologies Corporation Powder classification system and method

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2631968A (en) * 1953-03-17 Sheetsxsheet i
US2429436A (en) * 1944-08-31 1947-10-21 American Cyanamid Co Combined gravity classification and screening of ore
US2567207A (en) * 1947-01-21 1951-09-11 Houdry Process Corp Maintenance of catalytic activity in hydrocarbon conversion systems
US2688401A (en) * 1949-09-29 1954-09-07 Standard Oil Co Flotation of active catalyst from spent catalyst
FR1047751A (en) * 1951-05-29 1953-12-16 Cie De Fives Lille Pour Const Method and device for the separation of solid bodies of different densities within a suspension of dense product
US3541002A (en) * 1967-12-29 1970-11-17 Cities Service Res & Dev Co Particulate catalyst regeneration method
US3887455A (en) * 1974-03-25 1975-06-03 Exxon Research Engineering Co Ebullating bed process for hydrotreatment of heavy crudes and residua

Also Published As

Publication number Publication date
US4287088A (en) 1981-09-01
ZA802700B (en) 1981-06-24

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